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CN101622060B - Method and device for introducing additive materials - Google Patents

Method and device for introducing additive materials Download PDF

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Publication number
CN101622060B
CN101622060B CN2007800433148A CN200780043314A CN101622060B CN 101622060 B CN101622060 B CN 101622060B CN 2007800433148 A CN2007800433148 A CN 2007800433148A CN 200780043314 A CN200780043314 A CN 200780043314A CN 101622060 B CN101622060 B CN 101622060B
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CN
China
Prior art keywords
container
additive
feeding device
perhaps
particle
Prior art date
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Application number
CN2007800433148A
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Chinese (zh)
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CN101622060A (en
Inventor
G·温德林
M·哈克尔
K·费克廷杰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
EREMA Engineering Recycling Maschinen und Anlagen GesmbH
Original Assignee
EREMA Engineering Recycling Maschinen und Anlagen GesmbH
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Publication of CN101622060A publication Critical patent/CN101622060A/en
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    • B29K2105/06—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract

The invention relates to a method and a device for introducing and/or adding non-dry-powder additive materials and/or coating materials with a liquid, solid, semi-solid, or paste-like consistency or in suspended or emulsified form, for example, peroxides, fats, waxes, IV improvers, polymers, or similar materials, to an existing lumpy or particulate material which is moved and mixed, and optionally warmed and reduced to small pieces in a receptacle and/or compressor (1), said material being in particular polymer particles and/or flakes, wood fibers, paper cuttings, or similar materials. According to the invention, the additive material is introduced below the level of the material and/or material particles already in the receptacle (1).

Description

Introduce the method and apparatus of additive
The present invention relates to a kind of method and a kind of according to claim 10 device of be used for implementing the method for preamble of preamble according to claim 1.
There are some method and apparatus to can be used to liquid additive is ejected on the plastic material from the top under the known prior art condition, perhaps with fluidized bed process it added.
According to US 4,522,957 is described, in mixer liquid additive joined among the plastic pellet.
00/38895 pair of this method of WO is improved, and can reduce dust pollution or reduce dust to form, and at first with convective methods liquid additive is sprayed on the plastic pellet in the spray chamber, then carries out static mixing method.
Described according to EP 7624, in a kind of inert gas, liquid additive is joined among the plastic pellet.
Described according to WO 84/02530, at first in continuous mixer so that plastic pellet rotates, then under this rotation status, make it in air-flow, be stained with the high-temperature liquid state additive.
According to WO 9425509 disclosed a kind of methods, in agitating device by nozzle so that polymer particle is stained with liquid additive, in order to obtain better wettability effect, the surface of plastic pellet has inhomogeneous texture or makes it become coarse.
According to WO 2006/010291 described a kind of method and a kind of agitating device, liquid additive is injected on the plastic pellet in agitating device by injection apparatus, then so that mixture enter among the extruder.
EP 9817 also discloses a kind of method in addition, at first so that plastic pellet is stained with a kind of can the assurance liquid additive is distributed in plastic pellet lip-deep " coupling agent " or carrier better.Can be used as the especially paraffin of coupling agent or the material of class paraffin.
US 4,703 in addition, and 093 also discloses and a kind of liquid additive joined through the method among the plastic pellet of preheating.
DE 2631622 has described a kind of method of simultaneously pulverulent solids and liquid being sent into continuously among the handling machine.Realize this point by a nozzle ring, wherein so that liquid forms the overcoat of a hose-like, therein heart input solid matter.
But this method mainly at first is only applicable to the thin liquid shape additive that can atomize, and for the additive of the toughness additive of viscosity higher or solid or semi-solid property, effect is also insufficient.Usually only can be not exclusively, moistening unevenly plastic material.
If the additive of viscosity higher is heated to higher temperature, in order to can it be added with the thin liquid state, so usually understand in the temperature lower or colder apparatus surface formation additive deposit or coagulation.
This can cause metering difficulty and inaccuracy, and can polluting device.
Task of the present invention is, a kind of method and a kind of device are provided, can be in simple and uniform mode, the non-drying particulate shape additive of viscosity higher is joined among the bulk material, and especially join among plastic material or the polymer particle.Material surface can be stained with additive as far as possible fully, equably, and can evenly distribute or dispersing additive within the material particle.Can also add additive with correct dosage in addition, can avoid occurring deposit, thereby avoid polluting the also position of undesirable.
These tasks can be solved by claim 1 or 10 described features.
Adopt method of the present invention or device, can additive or coating be applied on bulk, the emboliform material very equably in useful mode, thereby realize the effect of complete wetted material particle surface.
In addition can accurate-metering the additive of trace extremely because all additive amount is introduced directly among the material particle, and the phenomenon of additive deposition can not appear.Especially additive does not come in contact with lower container or the reactor parts of any temperature, therefore can guarantee accurate-metering.The additive that do not have condensation or solidify pollute or be deposited in the reactor and the position of undesirable on, therefore do not need to carry out frequent clean.With from the top additive injection is compared to the known metering method on the material particle under the prior art condition, can significantly reduce even the dust that stops additive or contain additive condenses on the lower position of temperature.
The dynamic motion or rotatablely move of material particle in container helps on the surface with additive paint material particle, and is conducive to additive evenly be distributed or be distributed on the material particle.The mode that guarantees this effect is: the material particle is crossed or is rotated along the container side wall sideslip, and takes away by this way the additive that occurs here.
Therefore adopt the method for the present invention can moistening whole surface, and in the process of stirring particle so that additive distribute best.
Other advantage of the present invention can be consulted dependent claims.
Can dispose one or more feeding devices.These feeding devices all are arranged on the container side wall inboard, perhaps among the container side wall inner surface passes into container.
There is diverse ways to can be used to install, arrange feeding device.Useful especially mode is a plurality of feeding devices of configuration, for example can be arranged on the equal height of container bottom or stirring tool top, and preferably be evenly distributed in the circumferencial direction of container inner wall.
Another kind method is: arranged superposed about each feeding device is become vertical row, and the upwardly extending row that perhaps tilt can stagger or twist arrangement in case of necessity.Feeding device also can be particularly dispersedly or be evenly distributed in the container, perhaps only dispose a unique feeding device.
Feeding device suitably is arranged in the container, make it particularly be in the interior below, material thing position of container, thereby additive only can directly joins among the material particle of rotation all the time.Usually form the stirring eddy flow by the material particle in the motion of internal tank, schematically illustrated such as accompanying drawing 1.Advantageously in the process of carrying out whole method, edge or the thing position, the top of stirring eddy flow are positioned at the feeding device top.
Feeding device preferably is arranged in the material thing position in the container or stirs the height in 1/3rd zones, centre of eddy flow, so just additive can be evenly spread on the material particle.
If feeding device in the residing zone of container inside or the highly just material particle of motion or rotation applies zone or the height of maximum pressure to it, then especially favourable for the high additive of viscosity.So just can guarantee that distribution of material is good.Determine this zone or material oppose side wall applied pressure according to rotating speed, type, quantity and the shape of stirring tool.
Feeding device can be simple reinforced joint or the charge door on the container side wall, also can be the feed introduction form.Preferably by measuring pump gear pump or diaphragm pump is metered into or feeding additive for example.These pumps can be controlled the addition of additive.As previously mentioned, because all additives can be introduced directly among the material particle, therefore can be with very accurately and do not have lossy mode to measure.Avoided to a great extent the loss that causes because of similar phenomenons such as depositions.
For the interfering material particle is not in the motion of internal tank, feeding device preferably flushes with the inwall of container, and inwardly do not stretch into or reach internal tank.
The additive that joins among the material flows out from feeding device with droplet or pasty state form usually.The material particle moves along container inner wall under the positive action of stirring tool, contacts and produce friction with inwall.Directly taken away by the material particle by the additive that the feeding device straight line flows out, and in whipping process, distribute more equably.
For some additive, may need by additive wet pans wall, with this so that additive and material particle can disperse better.In order to realize this point, can dispose an additional independent heater, it only heats inboard or the container side wall of container side wall.This heater preferably is independent of temp. controllable or heatable stirring tool, perhaps is independent of other and is used for heater that the material in the container is heated.Can reduce the viscosity of additive by this way, thereby improve the flowability of additive, better the wet pans inwall.So just can be better with distribution of additives on the material particle.
Cause obstruction for fear of pasty state or full-bodied additive, feeding device itself and input pipe thereof or reservoir vessel also can be heatable.The wax that for example so can at room temperature add solid state wax or pasty state with abundant liquid form.Also can correspondingly adjust the pressure that imposes on additive in case of necessity, perhaps be used for the pressure of feeding additive, especially can highly select accordingly, in order to can add the additive of viscosity higher.
The suitable material of at high temperature processing perhaps keeps higher material temperature in principle because can reduce like this viscosity of additive, and distribute better, dispersion particle more equably.
Preferably can also avoid in addition the inwall by the additive wet pans, perhaps reduce moistening degree.For example can accomplish this point by the special decorative pattern of specific coatings or chamber wall.By this way can be so that the additive drop that is attached on the container inner wall be easier to break away from sidewall, thus be easier to be taken away by the material particle of material or motion, so that chamber wall can be by not moistening.
Other advantage of the present invention and design can be obtained by specification and accompanying drawing.
The present invention is schematically illustrated in the accompanying drawings by embodiment, hereinafter with reference to accompanying drawing the present invention is exemplarily illustrated.
The schematic diagram of accompanying drawing 1 device of the present invention.
Accompanying drawing 1 is depicted as the generalized section of device of the present invention.This device is existing various embodiment under the prior art condition.
The device of the cutting compacting machine form shown in the accompanying drawing 1 has container 1, is furnished with axis pulverizing or stirring tool 4 that rotate, that driven motor 5 drives around approximate vertical in its bottom.Be provided with opening with pulverizing and stirring tool 4 equal-height positions on the sidewall of container 1, the machine barrel 2 of screw extruder just is connected on this opening.The extruder screw 3 that has a driven motor 6 to drive in the machine barrel 2.The quilt that screw extruder is carried pulverize and the material that mixes especially plastics discharge from spiro rod machine tube by discharging opening 7.In the process of processing plastic material, at first fusing or plasticizing in extruder of material.Also can apply vacuum to container 1.
In container 1, put into the material that to process.Material is bulk or particle shape in container 1, therefore compare with its volume to have very large surface.Material is such as the thermoplastic material that can be the forms such as thin slice, particle, film rubbish.Well imagine it also can is the similar materials such as wood-fibred, newspaper.By stirring tool 4 so that the material particle in container 1 ceaselessly the motion or the rotation, thereby with the particle mixing, decide on the structure of stirring tool 4, can also pulverize in case of necessity and/or pre-compacted, also material can be heated, perhaps carry out drying or crystallization.Especially for plastic material, the motion of material particle in container 1 can so that plastic pellet in heating process, can not be bonded together, thereby keep the block characteristics of material.
The lower sidewall of this external container 1 also is furnished with the feeding device 10 of reinforced joint form, and this joint is passed into via opening among the container 1, and wherein said opening flushes with side wall inner surfaces, and feeding device 10 extend into internal tank without any part.One or more additives or coating can be metered among the container 1 by this feeding device 10.
Feeding device 10 is fit to add the additive of non-drying particulate shape, non-dry powdered, non-dried particles shape or non-dried crystals shape through suitably design.Usually add dry Powdered or particulate additive, similar substances such as pigment, filler from the top by simple loading hopper.Therefore can by feeding device 10 be metered into can pumping thin liquid or thick, solid-state, semisolid or the pasty state additive of viscosity higher especially.Feeding device 10 for example is fit to add thin liquid shape additive, and the additive of thickness such as plasticizer, peroxide perhaps also can add harder butyrous or dough shape additive, and for example fat or wax also can add polymer.So-called solid additives for example has wax or fat, although dimensionally stable at room temperature still can extend, be out of shape.Also can utilize in this way certain carrier solution to add additive or the inserts that is initially powdery, similar substances such as pigment, filler with dispersion, slurries, suspension or emulsion form.
As shown in Figure 1, feeding device 10 is arranged in the below of the rotation material particle thing position in the container 1, perhaps below stirring edge, eddy flow the top.Therefore be not for example by spray or splash into mode but sidewall by container 1 adds additive from the top.The material of motion skims over feeding device 10 or charge door all the time, thereby takes away the additive of outflow, it is applied on the material particle, and makes its dispersion or be distributed within the material particle.
The surface of material particle is larger, and then the peptizaiton of additive is better.
Decide on dilution factor, can pass through a kind of additive carrier in case of necessity, add additive, especially reactive additive according to 0.01～20% percentage by weight.For example when using the PET thin slice as raw material, can apply 0.2～0.6% additive.
The research on maximum utilized quantity of additive refers to material total surface or the moistening required consumption of material particle total surface in the container 1.
Type and reactivity thereof on additive are decided, and additive only just can react with material in extruder or melt in some cases.
Finally in extruder, material is melted fully, if necessary, also can filter and/or exhaust.
Can in one step, carry out method of the present invention, but also can be integrated among two steps or the multi-step process.Be preferably in the first step and in a preposition pretreating containers or first container 1, add additive.Feeding device can be arranged among this pretreating containers for this reason.Then in another container 1, continue to process material, and/or add other additive, also can carry out drying or crystallization in case of necessity.

Claims (19)

1. method of be used for introducing additive, be used in container or cutting compacting machine (1), moving, stir, through introducing in heating and the bulk of pulverizing or the particle shape material or adding liquid, solid-state, semisolid, pasty state, suspend or the emulsification form, non-drying particulate shape with viscosity higher, non-dry powdered additive or coating material, wherein below, the material thing position in container (1) adds additive, it is characterized in that the material particle of rotation applies the zone of maximum pressure or this height part adding additive of container (1) to the sidewall of container (1) in container (1).
2. method according to claim 1 is characterized in that, adds additive in 1/3rd zones, centre of the material thing position in container (1) or the formed stirring eddy flow that rotatablely moves.
3. method according to claim 2, it is characterized in that, add additive by one or more feeding devices (10), carry out feed by measuring pump, described feeding device is designed to charge door or burner design, is arranged on the inside sidewalls of container (1), perhaps passes sidewall and passes into, along circle distribution, perhaps stacked arrangement is in a row up and down at equal height.
4. method according to claim 3 is characterized in that, suitably keeps the thing position of the stirring eddy flow that passing through in material particle or the container (1) moves forms, and makes it be positioned at all the time the top of feeding device (10).
5. method according to claim 3, it is characterized in that, by or utilize along the inside sidewalls of container (1) and feeding device (10) and skim over or additive is taken away or introduced to the material particle that rotates, perhaps by this way additive is applied on the material particle.
6. method according to claim 1, it is characterized in that, before adding additive, perhaps in adition process, regardless of the material temperature in the container (1), the independent heating that all inboard or the sidewall of container (1) is added, so that the viscosity of the additive that reduces to add, and improve moistening degree.
7. method according to claim 1 is characterized in that, decides on dilution factor, by a kind of additive carrier, adds additive with the consumption with respect to 0.01～20% percentage by weight of end product gross weight.
8. method according to claim 1 is characterized in that, the maximum adding quantity of additive is exactly the required amount of material total surface in the wet pans (1).
9. method according to claim 1 is characterized in that, described bulk or particle shape material are polymer particle or polymer flake, wood-fibred, shredded paper.
10. be used for implementing the device of each described method of claim 1～9, have at least one container or cutting compacting machine (1), wherein being furnished with at least one can be around the stirring tool (4) of vertical axis rotation, be used for so that bulk to be processed or particle shape material enter motion or rotation status, material is stirred, heating, or pulverize, wherein dispose at least a feeding device (10) that is used for implementing each described method of claim 1～8, be used for adding liquid, solid-state, semisolid or pasty state, suspend or the emulsification form, non-drying particulate shape additive with viscosity higher, wherein feeding device (10) is arranged in the below, thing position of the material that is positioned at container (1) in the course of work, it is characterized in that feeding device (10) the material particle that move just in residing zone in container (1) applies the zone of maximum pressure to the sidewall of container (1).
11. device according to claim 10 is characterized in that, feeding device (10) is arranged on the inside sidewalls of container (1), perhaps takes shape on the sidewall of container (1) or passes among the container (1).
12. device according to claim 10 is characterized in that, feeding device (10) is evenly distributed on the equal height of inwall circumference of container (1), perhaps overlapping being arranged in a row up and down.
13. device according to claim 10, it is characterized in that, feeding device (10) in container (1) with the bottom or with stirring tool (4) be separated by certain altitude or distance, feeding device (10) is in this height/distance below the thing position that is positioned at material particle container (1) or rotation given in advance all the time, perhaps is in the material Particles Moving or rotates the below of formed stirring eddy flow thing position.
14. device according to claim 13 is characterized in that, feeding device (10) is disposed in the material in the container given in advance (1) or stirs the height in 1/3rd zones, centre of eddy flow.
15. device according to claim 10 is characterized in that, feeding device (10) is designed to outlet or burner design, and can utilize measuring pump to feed in raw material, and can be metered into additive with the droplet form.
16. device according to claim 10 is characterized in that, feeding device (10) flushes with the inwall of container (1), and is not from the interior side-prominent of container (1) or extend into the inside of container (1).
17. device according to claim 10, it is characterized in that, at least also dispose an independently heater, only it is used for inboard or the sidewall of independent heating container (1), and also can heat separately feeding device (10) and/or its input pipe or reservoir vessel, so that the viscosity of the additive that reduces to add, and the wettability effect on the sidewall of raising container (1).
18. device according to claim 10, it is characterized in that, adopt and apply anti-adhering coating, press the method for decorative pattern, so that the inner surface of container (1) becomes non-wetable surface, thereby reduce wettability, perhaps so that the inboard can be not moistening by the additive that is added institute.
19. device according to claim 10 is characterized in that, dispose a plurality of containers (1) according to successively putting in order and arranging, and feeding device (10) is disposed at least among the first container (1).
CN2007800433148A 2006-11-23 2007-11-22 Method and device for introducing additive materials Active CN101622060B (en)

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